Polyvinyl chloride compositions containing impact modifiers and calcium carbonate

Abstract

Provided are polyvinyl chloride profile compositions comprising (a) polyvinyl chloride having a K value of from K-63 to K-70, (b) an impact modifier, and (c) ground calcium carbonate having (i) a d 50 particle size value of 400 to 900 nm, (ii) a d 98 particle size value of less than 2.6 µm, and (iii) a ratio of particles having a d 50 particle size value to particles having a d 20 particle size value (d 50 / d 20 ) of less than 2.0.

Description

FIELD OF THE INVENTION

[0001] This invention relates generally to polyvinyl chloride profile compositions containing impact modifiers and calcium carbonate.BACKGROUND

[0002] Acrylic impact modifiers and calcium carbonate fillers are a critical component of polyvinyl chloride ("PVC") end use application such as window and technical profiles. Such components provide performance properties required of PVC composites, for example, gelation rate, processing rheology, gloss, color, and impact strength. Impact modifiers and calcium carbonate fillers as currently used in the industry can counteract each other, however, making it difficult to achieve a single formulation that exhibits sufficiently favorable performance in all of such properties.

[0003] Various impact modifiers and grades of calcium carbonate have been utilized in the industry for a variety of PVC products. For example, WO 2016 / 050698 A1 discloses certain PVC compositions containing acrylic impact modifiers and calcium carbonate.

[0004] See also, for example, EP 2628775 which refers to a mineral matter powder preparation by wet process without acrylic additive or other grinding aid additives and to the use of said mineral matter after an optional hydrophobic treatment. Said mineral material having superior dispersing properties

[0005] EP 2594605 relates to a thermoplastic composition comprising the melt blending product of one or more thermoplastic polymers; and from 2 to 20 PHR, of one or more gloss reducing additives wherein each gloss reducing additive comprises a (meth)acrylate copolymer having a glass transition temperature of greater than or equal to 40°C and 0.001 to 0.04 PHM derived from one or more crosslinking monomers and / or graft-linking agents having two or more ethylenically unsaturated radicals capable of free-radical polymerization, wherein a test specimen produced from the thermoplastic composition has one or more of the following properties: (a) a gloss less than 65, 75 degree angle and (b) a combination of a roughness according to DIN 4768 of Ra greater than or equal to 0.6 microns, Rz greater than or equal to 6 microns and Rmax greater than or equal to 7 microns, is provided. Methods for producing the thermoplastic compositions, methods for producing articles from the thermoplastic compositions and such articles are also provided.

[0006] In EP 1548058 thermoplastic polymer compositions are disclosed that can be processed into capstocks having a reduced gloss appearance, high impact strength and superior weatherability. The capstocks described are especially useful for extrusion into articles. They are also useful for application to various poor weathering structural plastic articles for preparing multi-layered composites having improved weatherability. Methods for manufacturing structural plastic capstocks and composites and articles produced therefrom having reduced gloss appearance are also described.

[0007] The prior art does not, however, disclose a PVC formulation according to the present invention, which achieves a synergy between specific calcium carbonates and impact modifiers.

[0008] Accordingly, there is a need to develop PVC formulations containing acrylic impact modifiers and calcium carbonate that do provide improvements in impact strength, processing rheology, gelation rate, gloss, and color.STATEMENT OF INVENTION

[0009] One aspect of the invention provides a polyvinyl chloride composition comprising (a) polyvinyl chloride having a K value of from K-63 to K-70, (b) a multistage acrylic impact modifier comprising (i) 65 to 96 weight % of a core polymer, based on the total weight of the multistage acrylic impact modifier, comprising polymerized units derived from (A) 95 to 99.9 weight % of one or more alkyl acrylate monomers, and (B) 0.1 to 1.5 weight % of one or more cross-linking monomers, graft-linking monomers, and combinations thereof, based on the total weight of the core, and (ii) 4 to 35 weight % of a shell polymer, based on the total weight of the multistage acrylic impact modifier, comprising polymerized units derived from (A) 95 to 100 weight % of one or more alkyl(meth)acrylate monomers, and (B) 0 to 1.5 weight % of one or more chain transfer agents, based on the total weight of the shell; and (c) ground calcium carbonate having (i) a d 50 particle size value of 400 to 900 nm, (ii) a d 98 particle size value of less than 2.6 µm, and (iii) a ratio of particles having a d 50 particle size value to particles having a d 20 particle size value (d 50 / d 20 ) of less than 2.0, wherein the d 20 , d 50 and d 98 values are determined by the sedimentation method as set out herein.BRIEF DESCRIPTION OF THE FIGURES

[0010] FIG. 1 shows the impact strength profiles of exemplary PVC profile compositions in accordance with the present invention and comparative PVC profile compositions. FIG. 2 shows the impact strength profiles of exemplary PVC profile compositions in accordance with the present invention and comparative PVC profile compositions. FIG. 3 shows the impact strength profiles of exemplary PVC profile compositions in accordance with the present invention and comparative PVC profile compositions. DETAILED DESCRIPTION

[0011] The inventors have now surprisingly found that polyvinyl chloride ("PVC") compositions according to the claims, containing polyvinyl chloride, impact modifiers, and ground calcium carbonate having (i) a d 50 particle size value of 400 to 900 nm, (ii) a d 98 particle size value of less than 2.5 µm, and (iii) a ratio of particles having a d 50 particle size value to particles having a d 20 particle size value (d 50 / d 20 ) of less than 2.0 provide significant improvements in impact strength, processing rheology, gloss, and color.

[0012] As used herein, the term "polymer" refers to a polymeric compound prepared by polymerizing monomers, whether of the same or a different type. The generic term "polymer" includes the terms "homopolymer," "copolymer," "terpolymer," and "resin." As used herein, the term "polymerized units derived from" refers to polymer molecules that are synthesized according to polymerization techniques wherein a product polymer contains "polymerized units derived from" the constituent monomers which are the starting materials for the polymerization reactions. As used herein, the term "(meth)acrylate" refers to either acrylate or methacrylate or combinations thereof, and the term "(meth)acrylic" refers to either acrylic or methacrylic or combinations thereof. As used herein, the term "substituted" refers to having at least one attached chemical group, for example, alkyl group, alkenyl group, vinyl group, hydroxyl group, carboxylic acid group, other functional groups, and combinations thereof. As used herein, the term "first polymeric stage" refers to any stage of the acrylic copolymer. It can be the only stage in a single stage polymer or the first, second, third, last, or any stage, chronologically, in a multistage polymer. As used herein, the term "second polymeric stage" refers to any other stage of the acrylic copolymer that is not the first stage. It can be the first, second, third, last, or any stage, chronologically, in a multistage polymer.

[0013] As used herein, the term "phr" means per hundred parts resin or polymer solids. As used herein, the term "molecular weight" or "weight average molecular weight" or "M w " refers to the weight average molecular weight of a polymer as measured by gel permeation chromatography ("GPC"), for acrylic polymers against polystyrene calibration standards following ASTM D5296-11 (2011), and using tetrahydrofuran ("THF") as the mobile phase and diluent. As used herein, the term "particle size" means the weight average particle size of the emulsion (co)polymer particles as measured using a Brookhaven BI-90 Particle Sizer.

[0014] As used herein, the terms "glass transition temperature" or "T g " refers to the temperature at or above which a glassy polymer will undergo segmental motion of the polymer chain. Glass transition temperatures of a copolymer can be estimated by the Fox equation (Bulletin of the American Physical Society, 1 (3) Page 123 (1956)) as follows: 1 / T g = w 1 / T g 1 + w 2 / T g 2 For a copolymer, w 1 and w 2 refer to the weight fraction of the two comonomers, and T g(1) and T g(2) refer to the glass transition temperatures of the two corresponding homopolymers made from the monomers. For polymers containing three or more monomers, additional terms are added (w n / T g(n) ). The glass transition temperatures of the homopolymers may be found, for example, in the "Polymer Handbook," edited by J. Brandrup and E.H. Immergut, Interscience Publishers. The T g of a polymer can also be measured by various techniques, including, for example, differential scanning calorimetry ("DSC"). As used herein, the phrase "calculated T g " shall mean the glass transition temperature as calculated by the Fox equation.

[0015] As used herein, the terms "d 20 ", "d 50 ", and "d 98 " particle size values refer to the size at which 20%, 50%, and 98%, respectively, of mass of agglomerated particles is accounted for by particles having a diameter less than or equal to the specified value. Thus, the d 50 value is the "weight median particle size" at which 50 weight % of all particles are smaller than the indicated particle size. As used herein, the term "d 50 / d 20 " refers to the ratio of particles having a d 50 particle size value to particles having a d 20 particle size value. The d 20 , d 50 , and d 98 values can be determined by various techniques, including, for example, by a Sedigraph ™< III Plus (available from Micromeritics Instrument Corporation) utilizing the sedimentation method (i.e., an analysis of sedimentation behavior in a gravimetric field).

[0016] The inventive PVC compositions comprise polyvinyl chloride, an impact modifier, and ground calcium carbonate, according to the claims. The polyvinyl chlorides of the inventive composition can be obtained by conventional suspension polymerization, emulsion polymerization, bulk polymerization, or solution polymerization in the presence of initiators. In certain embodiments, the polyvinyl chloride is present in the PVC profile composition in an amount of from 70 to 90 weight %, preferably of from 75 to 85 weight %, and more preferably of from 77 to 83 weight %, based on the total weight of the PVC profile composition. K-values are correlated with solution viscosities and molecular weights of PVC as set forth in ISO 1628 2:1998. The preferred K-value range is from K-63 to K-70, preferably of from K-64 to K-69, and more preferably of from K-65 to K-68.

[0017] The inventive PVC compositions comprise an impact modifier. In certain embodiments, the impact modifier is present in the PVC profile composition in an amount of from 1 to 8 phr, preferably of from 3 to 7 phr, and more preferably of from 4 to 6 phr, based on the total weight of the PVC profile composition. Suitable impact modifiers include, for example, methacrylate-butadiene-styrene copolymers ("MBS"), acrylonitrile-butadiene-styrene copolymers ("ABS"), chlorinated polyethylene ("CPE"), acrylic-grafted chlorinated polyethylene, acrylic-grafted PVC, and acrylic impact modifiers ("AIM").

[0018] Suitable multistage acrylic impact modifiers include, for example, those having a core-shell morphology comprising a core polymer and a shell polymer. In embodiments according to the invention, the core polymer is present in the multistage acrylic impact modifier in an amount of from 65 to 96 weight %, preferably 85 to 96 weight %, and more preferably of from 88 to 94 weight %, based on the total weight of the multistage acrylic impact modifier. In embodiments according to the invention, the shell polymer is present in the multistage acrylic impact modifier in an amount of from 4 to 35 weight %, preferably 5 to 15 weight %, and more preferably of from 6 to 12 weight %, based on the total weight of the multistage acrylic impact modifier. In certain embodiments, the multistage acrylic impact modifier comprises one or more intermediate layer polymers between the core polymer and the shell polymer.

[0019] The core of the multistage acrylic impact modifier comprises polymerized units derived from one or more alkyl acrylate monomers. The alkyl acrylate monomers comprise linear and branched alkyl acrylates wherein the alkyl group has from 1 to 12 carbon atoms. Suitable alkyl acrylate monomers include, for example, ethyl acrylate, butyl acrylate, 2-ethyl hexyl acrylate, cyclopentyl acrylate, cyclohexyl acrylate, benzyl acrylate, and isooctylacrylate. In certain preferred embodiments, the alkyl acrylate monomers of the cross-linked core comprise one or more of butyl acrylate and 2-ethylhexyl acrylate. In embodiments according to the invention, the alkyl acrylate monomers are present in the core in an amount of from 95 to 99.9 weight %, preferably of from 97 to 99.5 weight %, and more preferably of from 98 to 99 weight %, based on the total weight of the core.

[0020] The core of the multistage acrylic impact modifier further comprises polymerized units derived from one or more cross-linking monomers, graft-linking monomers, and combinations thereof. Suitable cross-linking and graft-linking monomers include, for example, butanediol di(meth)acrylate, ethylene glycol di(meth)acrylate, divinyl benzene, diethylene glycol di(meth)acrylate, diallyl maleate, ally acrylate, allyl methacrylate, diallyl phthalate, triallyl phthalate, and trimethylolpropane tri(meth)acrylate. In certain embodiments, the cross-linking monomers and graft-linking monomers of the cross-linked core comprise allyl methacrylate. In embodiments according to the invention, the cross-linking monomers and graft-linking monomers are present in the cross-linked core in an amount of from 0.1 to 1.5 weight %, preferably of from 0.2 to 1.0 weight %, and more preferably of from 0.3 to 0.8 weight %, based on the total weight of the core.

[0021] The shell of the inventive multistage acrylic impact modifier comprises one or more of alkyl(meth)acrylate monomers. The alkyl(meth)acrylate monomers comprise linear and branched alkyl(meth)acrylates wherein the alkyl group has from 1 to 12 carbon atoms. Suitable alkyl(meth)acrylate monomers include, for example, methyl methacrylate, ethyl acrylate, butyl acrylate, butyl methacrylate, 2-ethyl hexyl acrylate, cyclopentyl acrylate, cyclohexyl acrylate, benzyl acrylate, benzyl methacrylate, and isooctylacrylate. In certain preferred embodiments, the alkyl(meth)acrylate monomers of the shell comprise methyl methacrylate. In embodiments according to the invention, the alkyl(meth)acrylate monomers are present in the shell in an amount of from 95 to 100 weight %, preferably of from 96 to 99 weight %, and more preferably of from 97 to 98 weight %, based on the total weight of the shell.

[0022] In certain embodiments, the shell of the inventive multistage acrylic impact modifier further comprises polymerized units derived from one or more chain transfer agents. Suitable chain transfer agents include, for example, 1-dodecanethiol, t-dodecanethiol, thioethanol, hexanethiol, mercaptopropionic acid, methyl-3-mercaptopropionate, butyl-3-mercaptopropionate. In embodiments according to the invention, the chain transfer agents are present in the shell in an amount of from 0 to 1.5 weight %, preferably of from 0.05 to 1 weight %, and more preferably of from 0.1 to 0.5 weight %, based on the total weight of the shell.

[0023] In certain embodiments, the multistage acrylic impact modifier further comprises one or more intermediate layers between the core and shell, each of which independently contains polymerized units derived from the monomer compositions described above for the entirety of the core and shell polymers. The multistage acrylic impact modifier may contain, for example, one, two, three, four, or five intermediate layers. In certain embodiments, the one or more intermediate layers contains a compositional gradient between the sub-layers such that the T g transitions from a minimum to a maximum over the width of the entire first intermediate layer. In certain embodiments, the calculated T g transitions from a lower limit of -50°C, -40°C, -30°C, - 25°C, -15°C, or 0°C, to an upper limit of 70°C, 55°C, 35°C, or 15°C. While not wishing to be bound by theory, it is believed that the compositional gradient is achieved by the proper selection of and manner and timing of addition of monomers during the emulsion polymerization process used to prepare the first intermediate layer. A multistage polymerization process may be used during which monomers are added in stages, rather than all at once, to the emulsion polymerization reactor (or reactor vessel), permitting an interpenetration of one layer into adjacent layers resulting in a T g gradient over the first intermediate layer.

[0024] In certain embodiments, the multistage acrylic impact modifiers have a particle size in the range of from 100 to 500 nm, preferably of from 100 to 300 nm, more preferably of from 120 to 220 nm, and even more preferably of from 150 to 200 nm, as measured by a Brookhaven BI-90 Particle Sizer.

[0025] Suitable polymerization techniques for preparing the polymers contained in the inventive polymer compositions include, for example, emulsion polymerization and solution polymerization, preferably emulsion polymerization, as disclosed in U.S. Patent No. 6,710,161. Aqueous emulsion polymerization processes typically are conducted in an aqueous reaction mixture, which contains at least one monomer and various synthesis adjuvants, such as the free radical sources, buffers, and reductants in an aqueous reaction medium. In certain embodiments, a chain transfer agent may be used to limit molecular weight. The aqueous reaction medium is the continuous fluid phase of the aqueous reaction mixture and contains more than 50 weight % water and optionally one or more water miscible solvents, based on the weight of the aqueous reaction medium. Suitable water miscible solvents include, for example, methanol, ethanol, propanol, acetone, ethylene glycol ethyl ethers, propylene glycol propyl ethers, and diacetone alcohol. In certain embodiments, the aqueous reaction medium contains more than 90 weight % water, preferably more than 95 weight % water, and more preferably more than 98 weight % water, based on the weight of the aqueous reaction medium.

[0026] The inventive PVC compositions comprise calcium carbonate. Suitable calcium carbonate includes, for example, ground natural calcium carbonate ("GCC", as distinguished from precipitated calcium carbonate). In embodiments according to the invention, the ground calcium carbonate has a d 50 particle size value of from 400 to 900 nm, preferably from 400 to 800 nm, and more preferably from 400 to 700 nm. In embodiments according to the invention, the ground calcium carbonate has a d 98 particle size value of less than 2.6 µm, preferably less than 2.5 µm, and more preferably less than 2.4 µm. In embodiments according to the invention, the ground calcium carbonate has a ratio of particles having a d 50 particle size value to particles having a d 20 particle size value (d 50 / d 20 ) of less than 2.0, such as from 2.0 to 1.3, preferably from 1.8 to 1.4, and more preferably from 1.7 to 1.5. In certain embodiments, the ground calcium carbonate is present in the PVC profile composition in an amount of from 4 to 25 phr, preferably 5 to 20 phr, and more preferably of from 6 to 18 phr, based on the total weight of the PVC profile composition.

[0027] The PVC profile compositions of the present invention are readily prepared by dry-blending or compounding methods that are known in the art of PVC processing. For example, the polyvinyl chloride, acrylic impact modifiers, and ground calcium carbonate of the present invention can be blended and processed using high-speed hot / cold mixers, and / or co-kneader extruders.

[0028] In certain embodiments, the inventive PVC profile compositions further comprise TiO 2 . Suitable grades of TiO 2 include, for example a rutile grade TiO 2 . In certain embodiments, the TiO 2 is present in the PVC profile composition in an amount of from 3 to 10 phr, preferably from 3.5 to 8 phr, and more preferably from 4 to 6 phr, based on the total weight of the PVC profile composition.

[0029] The inventive polymer compositions may also contain other optional ingredients that include, for example, thermal stabilizers, plasticizers, antioxidants, UV absorbers and light stabilizers, dyes, pigments, flame retardant agents, and other additives to prevent, reduce, or mask discoloration or deterioration caused by heating, aging, or exposure to light or weathering. The amount of optional ingredients effective for achieving the desired property provided by such ingredients can be readily determined by one skilled in the art.

[0030] As noted above, the PVC profile compositions of the present invention have end use applications including, for example, as for use in window profiles, pipes, technical profiles, wall panels, ceiling panels, cladding panels, or wire insulation. The inventive PVC profile compositions can be processed into a film and / or sheet by way of extrusion, calendering, or injection molding.

[0031] Some embodiments of the invention will now be described in detail in the following Examples.EXAMPLES Example 1 Particle Size Characterization of Exemplary and Comparative Ground Calcium Carbonate

[0032] Exemplary ground calcium carbonate for use in PVC profile compositions in accordance with the present invention and comparative calcium carbonate for use in comparative PVC profile compositions have the particle size properties as recited in Table 1. Table 1. Characterization of Exemplary and Comparative Calcium Carbonate Sample d 50 (µm) d 98 (µm) d 50 / d 20 CaCO 3 -A 0.602.31.64CaCO 3 -B* 0.8552.27*Comparative

[0033] The d 20 , d 50 , and d 98 values were determined by a Sedigraph ™< III Plus available from Micromeritics Instrument Corporation.Example 2 Preparation of Exemplary PVC Profile Compositions

[0034] Exemplary PVC profile compositions in accordance with the present invention contain the components recited in Table 2. Table 2. Exemplary PVC Profile Compositions S-PVC K-67 1< Ca / Zn OP 2< Acrylic Impact Modifier 1 Acrylic Impact Modifier 2 CaCO 3 -A 4< TiO 2 Sample [KM-376L 3< ] [KM-370 3< ] [KRONOS -CL 2220 5< ] (phr) (phr) (phr) (phr) (phr) (phr) E1 1003.56.0--8.04.0E2 1003.5--6.08.04.0E3 1003.5--6.016.04.0E4 1003.55.2--10.04.0E5 1003.54.5--10.04.0E6 1003.53.6--10.04.0E7 1003.55.2--7.04.0E8 1003.54.5--7.04.0E9 1003.53.6--7.04.0E10 1003.55.2--4.04.0E11 1003.54.5--4.04.0E12 1003.53.6--4.04.0E13 1003.55.2--12.04.0Available from Shin Etsu 2< Available from Chemson (Oyak Group) 3< Available from The Dow Chemical Company 4< Available from Omya 5< Available from KRONOS

[0035] All compositions were prepared by dry-blending using a high speed hot / cold mixer. All compositions were heated to 120°C and mixed in the hot mixer for about 6 minutes at 2600-3200 rpm, and then cooled to a temperature of 40°C and mixed in the cold mixer for about 6 minutes at 600 to 1100 rpm.Example 3 Preparation of Comparative PVC Profile Compositions

[0036] Comparative PVC profile compositions contain the components recited in Table 3. Table 3. Comparative PVC Profile Compositions S-PVC K-67 1< Ca / Zn OP 2< Acrylic Impact Modifier 1 Acrylic Impact Modifier 2 CaCO 3 -B 4< TiO 2 [KRONOS -CL 2220 5< ] Sample [KM-376L 3< ] [KM-370 3< ] (phr) (phr) (phr) (phr) (phr) (phr) C1 1003.55.2--7.04.0C2 1003.55.2--10.04.0C3 1003.55.2--12.04.0C4 1003.5--6.08.04.0C5 1003.56.0--8.04.0C6 1003.5--6.016.04.0C7 1003.5----104.0C8 1003.55.2----4.0 1< Available from Shin Etsu 2< Available from Chemson (Oyak Group) 3< Available from The Dow Chemical Company 4< Available from Omya 5< Available from KRONOS

[0037] All compositions were prepared by dry-blending using a high speed hot / cold mixer. All compositions were heated to 120°C and mixed in the hot mixer for about 6 minutes at 2600-3200 rpm, and then cooled to a temperature of 40°C and mixed in the cold mixer for about 6 minutes at 600 to 1100 rpm.Example 4 Impact Strength Characterization of Exemplary PVC Profile Compositions

[0038] The single-V notch-Charpy impact strength (measured per ISO 179-1 / 1eC) of inventive PVC profile compositions as prepared in Example 2 was evaluated as shown in Table 4. Table 4. Impact Strength of Inventive PVC Profile Compositions Sample Impact Strength (KJ / m 2< ) Brittle Break (%) Wall Thickness (mm) E1 45.7 ± 12.4302.95 ± 0.05E2 14.8 ± 0.41002.99 ± 0.01E3 62.8 ± 1.202.89 ± 0.01E4 68.3 ± 3.502.89 ± 0.01E5 66.3 ± 2.302.83 ± 0.01E6 15.8 ±1.41002.75 ± 0.12E7 65.5 ± 1.302.86 ± 0.01E8 15.7 ± 1.41002.85 ± 0.01E9 12. 9 ± 0.51002.94 ± 0.01E10 21.3 ± 8.2902.81 ± 0.01E11 14.7 ± 1.01002.82 ± 0.01E12 13.5 ± 0.51002.71 ± 0.01E13 68.6 ± 0.602.96 ± 0.02

[0039] All samples were evaluated according to the ISO 179-1 / 1eC impact test, with Charpy sample specimens having a 50 mm x 6 mm x the wall thickness reported in Table 4.Example 5 Impact Strength Characterization of Comparative PVC Profile Compositions

[0040] The single-V notch-Charpy impact strength (measured per ISO 179-1 / 1eC) of comparative PVC profile compositions as prepared in Example 3 was evaluated as shown in Table 5. Table 5. Impact Strength of Comparative PVC Profile Compositions Sample Impact Strength (KJ / m 2< ) Brittle Break (%) Wall Thickness (mm) C1 12.3 ± 0.41002.92 ± 0.02C2 12.8 ± 0.61003.01 ± 0.01C3 12.2 ± 0.51002.92 ± 0.01C4 11.3 ± 0.31003.00 ± 0.02C5 12.9 ± 0.51002.98 ± 0.03C6 13.3 ± 0.41002.96 ± 0.02C7 9.8 ± 0.41002.82 ± 0.01C8 14.0 ± 1.21002.71 ± 0.01

[0041] The impact strength characterization was carried out in accordance with the procedures described in Example 4.Example 6 Impact Strength Profile Comparison of Exemplary and Comparative PVC Profile Compositions

[0042] FIG. 1 shows the impact strength profiles of inventive examples E7, E4, and E13 as determined in Example 4 compared against comparative examples C1, C2, and C3 as determined in Example 5. The data demonstrates that PVC profile compositions prepared in accordance with the present invention provide an unexpected increase in impact strength.

[0043] FIG. 2 shows the impact strength profiles of inventive examples E1 and E2 as determined in Example 4 compared against comparative examples C4 and C5 as determined in Example 5. The data demonstrates that PVC profile compositions prepared in accordance with the present invention provide an unexpected increase in impact strength.

[0044] FIG. 3 shows the impact strength profiles of inventive examples E2 and E6 as determined in Example 4 compared against comparative examples C4 and C6 as determined in Example 5. The data demonstrates that PVC profile compositions prepared in accordance with the present invention provide an unexpected increase in impact strength.Example 7 Extrusion Characterization of Inventive and Comparative PVC Profile Compositions

[0045] The extrusion characterization of inventive and comparative PVC profile compositions was carried out using a conical twin-screw extruder, fitted with a rectangular profile die, using the extrusion conditions presented in Table 6. Table 6. Extruder Conditions Screw Set Temperatures Speed (rpm) Temp (°C) Barrel 1 (°C) Barrel 2 (°C) Die 1 (°C) Die 2 (°C) Die 3 (°C) 30150170170190190190

[0046] The extrusion characteristics of inventive PVC profile compositions as prepared in Example 2 were evaluated as shown in Table 7. Table 7. Extrusion Characteristics of Inventive PVC Profile Compositions Sample Torque (amps) Melt Pressure and Temperature Output (kg / hr) Pressure P1 before vent (mPa) Pressure P2 after vent (mPa) Die Pressure P head (mPa) Temp Melt (°C) Head Melt (°C) E1 3.641.111.220.315817111.2E2 3.480.69.320.715617110.6E3 3.550.99.922.015617210.6E4 3.660.911.321.815617210.7E5 3.540.710.021.215517110.5E6 3.440.79.020.915417110.4E7 3.570.911.021.415717110.6E8 3.500.710.121.215517110.5E9 3.530.810.521.215517110.8E10 3.430.89.420.615517010.2E11 3.400.79.020.515517010.3E12 3.250.56.118.61541709.3E13 3.600.911.021.515817211.2

[0047] The extrusion characteristics of comparative PVC profile compositions as prepared in Example 3 were evaluated as shown in Table 8. Table 8. Extrusion Characteristics of Comparative PVC Profile Compositions Melt Pressure and Temperature Sample Torque (amps) Pressure P1 before vent (mPa) Pressure P2 after vent (mPa) Die Pressure P head (mPa) Temp Melt (°C) Head Melt (°C) Output (kg / hr) C1 3.580.99.919.715717110.7C2 3.721.011.520.815917211.3C3 3.741.112.021.215917211.2C4 3.601.011.120.915717111.1C5 3.651.111.320.715817211.1C6 3.600.910.722.315617210.8C7 3.260.46.320.015117010.5C8 3.150.54.818.61531698.9

[0048] The extrusion data demonstrates that the extrusion characteristics of the inventive PVC profile compositions perform at least as good as those prepared with the comparative PVC profile compositions. Both the extruder torque and melt pressure increase as addition levels of impact modifiers and GCC in the compositions increase.Example 9 Gloss and Color Characterization of Inventive and Comparative PVC Profile Compositions

[0049] The gloss and color characteristics of inventive and comparative PVC profile compositions was measured on the surface of extruded profiles, according to the ISO 7724 Standard, using a BYK Spectro-Guide, model 6834.

[0050] The gloss and color characterization of inventive PVC profile composition as prepared in Example 2 were evaluated as shown in Table 9. Table 9. Gloss and Color Characterization of Inventive PVC Profile Compositions Sample Gloss Unit (60°) L* a* b* E1 43.995.17-0.023.41E2 50.794.76-0.013.51E3 49.494.49-0.004.55E4 49.794.77-0.213.66E5 46.495.17-0.063.40E6 43.995.22-0.073.40E7 47.695.18-0.143.33E8 45.195.24-0.093.18E9 42.895.26-0.063.07E10 39.495.44-0.082.94E11 38.395.41-0.082.90E12 39.095.02-0.173.03E13 50.295.00-0.013.95

[0051] The gloss and color characterization of comparative PVC profile composition as prepared in Example 3 were evaluated as shown in Table 10. Table 10. Gloss and Color Characterization of Comparative PVC Profile Compositions Sample Gloss Unit (60°) L* a* b* C1 31.994.45-0.013.19C2 37.194.29-0.103.55C3 34.594.30-0.013.73C4 38.594.76-0.064.00C5 38.394.52-0.063.41C6 32.594.410.064.64C7 25.195.03-0.083.22C8 22.895.25-0.142.59

[0052] The data demonstrates that PVC profile compositions prepared in accordance with the present invention provides an unexpected boost with respect to the gloss of extruded profiles when compared against comparative PVC profile compositions. The better color consistency of the inventive PVC profile compositions as compared against comparative PVC profile compositions indicates that a wider extruder-processing window is achieved by compositions according to the present invention.

Claims

1. A polyvinyl chloride composition comprising: (a) polyvinyl chloride having a K value of from K-63 to K-70; (b) a multistage acrylic impact modifier comprising (i) 65 to 96 weight % of a core polymer, based on the total weight of the multistage acrylic impact modifier, comprising polymerized units derived from (A) 95 to 99.9 weight % of one or more alkyl acrylate monomers, and (B) 0.1 to 1.5 weight % of one or more cross-linking monomers, graft-linking monomers, and combinations thereof, based on the total weight of the core, and (ii) 4 to 35 weight % of a shell polymer, based on the total weight of the multistage acrylic impact modifier, comprising polymerized units derived from (A) 95 to 100 weight % of one or more alkyl(meth)acrylate monomers, and (B) 0 to 1.5 weight % of one or more chain transfer agents, based on the total weight of the shell; and (c) ground calcium carbonate having (i) a d50 particle size value of 400 to 900 nm, (ii) a d98 particle size value of less than 2.6 µm, and (iii) a ratio of particles having a d50 particle size value to particles having a d20 particle size value (d50 / d20) of less than 2.0; wherein the d20, d50 and d98 values are determined by the sedimentation method as set out in the description.

2. The composition of claim 1, wherein (i) the one or more alkyl acrylate monomers of the core are selected from the group consisting of ethyl acrylate, butyl acrylate, 2-ethyl hexyl acrylate, cyclopentyl acrylate, cyclohexyl acrylate, benzyl acrylate, and isooctylacrylate, and combinations thereof, and the one or more cross-linking monomers, graft-linking monomers, and combinations thereof of the core are selected from the group consisting of butanediol di(meth)acrylate, ethylene glycol di(meth)acrylate, divinyl benzene, diethylene glycol di(meth)acrylate, diallyl maleate, ally acrylate, allyl methacrylate, diallyl phthalate, triallyl phthalate, trimethylolpropane tri(meth)acrylate, and combinations thereof; and (ii) the one or more alkyl(meth)acrylate monomers of the shell are selected from the group consisting of methyl methacrylate, ethyl acrylate, butyl acrylate, butyl methacrylate, 2-ethyl hexyl acrylate, cyclopentyl acrylate, cyclohexyl acrylate, benzyl acrylate, benzyl methacrylate, isooctylacrylate, and combinations thereof, and the one or more chain transfer agents are selected from the group consisting of 1-dodecanethiol, t-dodecanethiol, thioethanol, hexanethiol, mercaptopropionic acid, methyl-3-mercaptopropionate, butyl-3-mercaptopropionate, and combinations thereof.

3. The composition of claim 1, wherein (i) the one or more alkyl acrylate monomers of the core are selected from the group consisting of butyl acrylate, 2-ethylhexyl acrylate, and combinations thereof, and the one or more cross-linking monomers, graft-linking monomers, and combinations thereof of the core is allyl methacrylate; and (ii) the one or more alkyl(meth)acrylate monomers of the shell is methyl methacrylate.

4. The composition of claim 1, wherein the impact modifier (b) is present in an amount of from 1 to 8 phr, based on the total weight of the polyvinyl chloride profile composition, and wherein the ground calcium carbonate (c) is present in an amount of from 4 to 25 phr, based on the total weight of the polyvinyl chloride profile composition.

5. The composition of claim 1, wherein the impact modifier (b) is present in an amount of from 4 to 6 phr, based on the total weight of the polyvinyl chloride profile composition, and wherein the ground calcium carbonate (c) is present in an amount of from 6 to 16 phr, based on the total weight of the polyvinyl chloride profile composition.

6. The composition of claim 1, wherein the polyvinyl chloride has a K value of from K-65 to K-68.

7. An article of manufacture comprising the polyvinyl chloride composition of claim 1, wherein the article of manufacture is selected from the group consisting of window profiles, pipes, technical profiles, wall panels, ceiling panels, cladding panels, or wire insulation.

8. The composition of claim 1, wherein the impact modifier is selected from the group consisting of methacrylate-butadiene-styrene copolymers, acrylonitrile-butadiene-styrene copolymers, chlorinated polyethylene, acrylic-grafted chlorinated polyethylene, acrylic-grafted PVC, acrylic impact modifiers, and combinations thereof.

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